JP2011511703A5 - - Google Patents

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Publication number
JP2011511703A5
JP2011511703A5 JP2010543360A JP2010543360A JP2011511703A5 JP 2011511703 A5 JP2011511703 A5 JP 2011511703A5 JP 2010543360 A JP2010543360 A JP 2010543360A JP 2010543360 A JP2010543360 A JP 2010543360A JP 2011511703 A5 JP2011511703 A5 JP 2011511703A5
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JP
Japan
Prior art keywords
sludge
drying
dried
dry
dewatered
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Pending
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JP2010543360A
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Japanese (ja)
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JP2011511703A (en
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Publication date
Priority claimed from CN2008100260395A external-priority patent/CN101224912B/en
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Publication of JP2011511703A publication Critical patent/JP2011511703A/en
Publication of JP2011511703A5 publication Critical patent/JP2011511703A5/ja
Pending legal-status Critical Current

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Description

【図2】

Figure 2011511703
[Figure 2]
Figure 2011511703

Claims (3)

下記のステップを含む汚泥乾燥の方法であって、
(1)乾燥した汚泥、焼却灰、粘土を直接に汚泥乾燥用担体とする。
(2)汚泥乾燥用担体と乾燥する脱水汚泥をそれぞれ攪拌混合装置に移送し攪拌混合を行う。
(3)混合汚泥を乾燥装置に移送し、乾燥する。
(4)ステップ(2)及びステップ(3)を繰り返す;
前記ステップ(3)において乾燥装置から排出した乾燥した汚泥は、;乾燥のために必要とする汚泥乾燥用担体の量によって決められる量が、取り出され、攪拌混合装置に移送し、乾燥する脱水汚泥と攪拌混合を行い、そして、乾燥装置に移送し乾燥し、残余部分の乾燥した汚泥は、汚泥乾燥の担体とし、別の攪拌混合装置に移送し、乾燥する脱水汚泥と攪拌混合を行い、最終の汚泥乾燥完成品を形成することを特徴とする請求項1に記載の汚泥乾燥の方法。
A method of drying sludge comprising the following steps,
(1) Dry sludge, incinerated ash, and clay are directly used as sludge drying carriers.
(2) The sludge drying carrier and the dehydrated sludge to be dried are each transferred to a stirring and mixing device and stirred and mixed.
(3) The mixed sludge is transferred to a drying device and dried.
(4) Repeat step (2) and step (3);
Step (3) dry sludge discharged odor Te from Drying apparatus; amount determined by the amount of carrier for drying sludge that required for drying is extracted and transported to a stirring and mixing apparatus, and dried Mix and mix with dewatered sludge, transfer to a drying device and dry, and dry the remaining sludge as a sludge drying carrier, transfer to another stirring and mixing device and mix with the dewatered sludge to be dried. 2. The method for drying sludge according to claim 1, wherein the final sludge drying finished product is formed.
上記ステップ()の乾燥する脱水汚泥の含水率は、51〜69%(W/W)であることを特徴とする請求項1、2又は3に記載の汚泥乾燥の方法。
The method for drying sludge according to claim 1, 2 or 3, wherein the moisture content of the dewatered sludge to be dried in the step ( 1 ) is 51 to 69% (W / W).
上記ステップ()中の脱水汚泥は、水処理から生じた汚泥と、湖、池、河川、大きな川、溝渠、排水管からの底泥と、軽化学工業及び食品加工から生産された汚泥を脱水することによって得られることを特徴とする請求項1、2又は3に記載の汚泥乾燥の方法。
The dewatered sludge in the above step ( 1 ) includes sludge generated from water treatment, sludge from lakes, ponds, rivers, large rivers, troughs, drainage pipes, and sludge produced from light chemical industry and food processing. The method for drying sludge according to claim 1, 2 or 3, wherein the method is obtained by dehydration.
JP2010543360A 2008-01-25 2008-05-28 Sludge drying method Pending JP2011511703A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN2008100260395A CN101224912B (en) 2008-01-25 2008-01-25 Method for drying sludge
PCT/CN2008/071117 WO2009094868A1 (en) 2008-01-25 2008-05-28 A method for drying sludge

Publications (2)

Publication Number Publication Date
JP2011511703A JP2011511703A (en) 2011-04-14
JP2011511703A5 true JP2011511703A5 (en) 2015-02-05

Family

ID=39857154

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2010543360A Pending JP2011511703A (en) 2008-01-25 2008-05-28 Sludge drying method

Country Status (7)

Country Link
US (1) US8387275B2 (en)
EP (1) EP2236467A4 (en)
JP (1) JP2011511703A (en)
CN (1) CN101224912B (en)
AU (1) AU2008349041B2 (en)
CA (1) CA2712822C (en)
WO (1) WO2009094868A1 (en)

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